Keeping gas pressure where it belongs
A fuel gas pipe must deliver enough gas to every appliance without dropping the pressure below what the burners need. NFPA 54 and the IPC let designers size low-pressure systems so the total pressure loss stays within a small allowance — commonly 0.3 inches of water column (in WC). This calculator computes the drop through a pipe segment so you can confirm a run is large enough before it goes in the wall.
How it works — the Spitzglass formula
For low-pressure gas (under about 1.5 psi) the code references the Spitzglass formula. Its
low-pressure form relates flow to the square root of diameter to the fifth power
times pressure drop, divided by length and specific gravity, with a
diameter-dependent friction factor Cr = 1 / sqrt(1 + 3.6/D + 0.03·D). Solving
for the pressure drop gives:
H = ( Q / (3550 · Cr) )^2 · ( Cg · L ) / D^5
where H is the drop in inches of water column, Q is flow in SCFH, D is the
actual inside diameter in inches, Cg is gas specific gravity (0.60 for natural
gas, 1.52 for propane), and L is length in feet. The tool uses Schedule 40
steel inside diameters and back-calculates the heat input from your flow using
the gas heating value (approximately 1,030 BTU/scf for natural gas and 2,516 BTU/scf for propane).
Worked example
Say you have a furnace drawing 100,000 BTU/h and a water heater drawing 40,000 BTU/h on the same branch — total load 140,000 BTU/h. Converting to SCFH for natural gas: 140,000 ÷ 1,030 ≈ 136 SCFH. The branch is 30 ft of 3/4-inch Schedule 40 pipe (inside diameter 0.824 in).
Plugging into the Spitzglass formula with Cg = 0.60:
Cr = 1 / sqrt(1 + 3.6/0.824 + 0.03×0.824)≈ 0.424H = (136 / (3550 × 0.424))^2 × (0.60 × 30) / 0.824^5- This works out to roughly 0.22 in WC — comfortably under the 0.3 in WC limit.
Extend that branch to 60 ft and the drop roughly doubles to about 0.44 in WC, exceeding the allowance. The fix is to upsize to 1-inch pipe (ID 1.049 in), which drops the loss well below 0.1 in WC.
Key design rules
- Pressure drop scales with the square of flow and linearly with length. Doubling the flow quadruples the drop; doubling the run length doubles it.
- Add equivalent length for fittings. An elbow typically adds 1–2 ft of equivalent length per nominal diameter; a tee can add more. Include these in the length you enter.
- Check the longest path, not each segment in isolation. The total drop from the meter to the farthest appliance is what must stay within the 0.3 or 0.5 in WC allowance.
- Manifold pressure matters. Natural gas appliances typically need about 3.5 in WC at the appliance manifold; propane appliances need about 11 in WC. If supply pressure minus the calculated drop still clears these values, the sizing is adequate.
- Propane runs through smaller pipes. Because propane has a higher heating value per cubic foot, the SCFH flow is much lower for the same BTU/h load, so propane systems often size down one nominal pipe size compared to natural gas for the same appliance load.